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公开(公告)号：US20190276753A1
公开(公告)日：2019-09-12
申请号：US16299008
申请日：2019-03-11
发明人： Mainak SARKAR , Nayan DAS , Ganesh Vitthalrao BUTLEY , Sarvesh KUMAR , Rama Kant YADAV , Pastagia Kashyapkumar MAHINDRA , Madhusudan SAU , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
摘要： The present invention relates to a process for production of High-Octane Gasoline blending component, Heavy Naphtha with high aromatic content and High Cetane Diesel from high aromatic middle distillate range boiling streams obtained from catalytic as well as thermal cracker units.
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公开(公告)号：US20220135890A1
公开(公告)日：2022-05-05
申请号：US17520455
申请日：2021-11-05
发明人： Nayan DAS , Mainak SARKAR , Ganesh Vitthalrao BUTLEY , Ramesh KARUMANCHI , Sarvesh KUMAR , Madhusudan SAU , Gurpreet Singh KAPUR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： C10G65/12
摘要： The present invention discloses an integrated process scheme for producing (i) high-octane gasoline blending stream (ii) high aromatic heavy naphtha stream which is a suitable feedstock for benzene, toluene, and xylene (BTX) production and (iii) high cetane ultra-low sulphur diesel (ULSD) stream suitable for blending in refinery diesel pool.
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公开(公告)号：US20230331645A1
公开(公告)日：2023-10-19
申请号：US18133953
申请日：2023-04-12
发明人： Nayan DAS , Mainak SARKAR , Ganesh Vitthalrao BUTLEY , Kalicharan CHATTOPADHYAY , Sarvesh KUMAR , Madhusudan SAU
CPC分类号： C07C2/864 , B01J29/166 , B01J21/04 , C07C2529/16 , C07C2529/14
摘要： A process for the upgrading of hydrocarbon streams, i.e., processing any hydrocarbon feed streams rich in benzene and sulphur compounds. The process for simultaneous hydrodesulfurization and benzene conversion to higher alkylated aromatic molecules (C7 to C10 aromatics), without need of prior treatment like distillation, or sulfur removal. The hydrocarbon feed streams are processed over sulfided metal catalyst impregnated on acid support simultaneously desulfurizes and alkylates the benzene molecules.
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公开(公告)号：US20220098130A1
公开(公告)日：2022-03-31
申请号：US17448965
申请日：2021-09-27
发明人： Vasamsetty Naga Veera HIMA BINDU , Mainak SARKAR , Ganesh Vitthalrao BUTLEY , Ajay KUMAR , Sujit MONDAL , Ramesh KARUMANCHI , Sarvesh KUMAR , Madhusudan SAU , Gurpreet Singh KAPUR , Sankara Sri Venkata RAMAKUMAR
摘要： The present invention provides a novel route for synthesis and production of linear alpha olefins (LAO) and central olefins from the feedstock comprising fatty acids, triglycerides and esters of fatty acids, and mixture thereof through controlled hydrogenolysis, hydrogenation and dehydration reactions simultaneously in a hydro processing reactor containing a catalyst system having dual site—a metallic site for hydrogenation/reduction reaction under hydrogen environment, and an acidic site for conversion of alcohol to olefin via E1 or E2 reaction mechanism.
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5.发明申请公开(公告)号：US20170058212A1
公开(公告)日：2017-03-02
申请号：US15239363
申请日：2016-08-17
发明人： Pravesh KUMAR , Pappu NARESH , Vinay Kumar CHAUDHARY , Darshankumar Manubhai DAVE , Kamal KUMAR , Murugan BALASUNDARAM , Karumanchi RAMESH , Ganesh Vitthalrao BUTLEY , Om Prakash NANDWANI , Madhusudan SAU , Brijesh KUMAR , Biswapriya DAS
IPC分类号： C10G67/00
摘要： This invention relates to a process for hydro cracking of heavy oils. More particularly, this invention relates to a catalytic process for converting heavy oils, such as vacuum gas oil (VGO) and VGO containing a high proportion of vacuum resid (VR) to middle distillate products.
摘要翻译： 本发明涉及重油加氢裂化方法。 更具体地说，本发明涉及一种用于将重油（例如真空瓦斯油（VGO））和含有高比例真空渣油（VR）的VGO转化成中间馏分产物的催化方法。
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公开(公告)号：US20190276752A1
公开(公告)日：2019-09-12
申请号：US16294771
申请日：2019-03-06
发明人： Mainak SARKAR , Darshankumar Manubhai DAVE , Ganesh Vitthalrao BUTLEY , Ramesh KARUMANCHI , Arun ARANGARASU , Sarvesh KUMAR , Madhusudan SAU , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： C10G67/02
摘要： The present invention relates to an assorted co-staging and counter stage hydro-treating process configuration scheme is disclosed for deep desulfurization and deep hydro-treating of diesel range hydrocarbons for obtaining diesel product having product sulfur less than 10 ppm and cetane number more than 51.
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公开(公告)号：US20190100705A1
公开(公告)日：2019-04-04
申请号：US16118332
申请日：2018-08-30
发明人： Mainak SARKAR , Darshankumar Manubhai DAVE , Ramesh KARUMANCHI , Madhusudan SAU , Ganesh Vitthalrao BUTLEY , Nepal VISHWAKARMA , Kamal KUMAR , Pravesh KUMAR , Sarvesh KUMAR , Debasis BHATTACHARYYA , Sanjiv Kumar MAZUMDAR , Sankara Sri Venkata RAMAKUMAR
IPC分类号： C10G47/24
摘要： The present invention relates to a hydrocracking reactor system and a process utilizing the same for upgrading heavy hydrocarbonaceous material to value-added products. Accordingly, an aspect of the present invention includes dispersing a liquid feedstock pre-mixed with a catalyst from top of a reactor vessel to obtain dispersed droplets having a predetermined droplet size less than 500 μm, introducing a gaseous feed comprising primarily of hydrogen from bottom of the reactor vessel to form a continuous gaseous phase throughout a cross-section of the reactor vessel, and allowing the dispersed droplets to contact the continuous gaseous phase throughout the cross-section of the reactor vessel to form reaction effluent comprising one or more lighter product hydrocarbons. The method may further include removing at least a top portion and at least a bottom portion of the reaction effluent from the reactor vessel.
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公开(公告)号：US20170128929A1
公开(公告)日：2017-05-11
申请号：US15232695
申请日：2016-08-09
发明人： Brijesh KUMAR , Pravesh KUMAR , Kamal KUMAR , Ganesh Vitthalrao BUTLEY , Madhusudan SAU , Biswapriya DAS
CPC分类号： B01J37/086 , B01J23/28 , B01J23/745 , B01J23/883 , B01J35/0013 , B01J37/18 , B01J37/20 , C01B32/20 , C10G47/02 , C10G47/26 , C10G65/12 , C10G2300/202 , C10G2300/205 , C10G2300/703
摘要： The present invention discloses a catalyst and process for hydrocracking of heavy hydrocarbon oils having majority portion boiling above 525° C. in the presence of hydrogen. A process comprising first step of converting heavy oil into lighter products in the presence of catalyst and hydrogen in slurry phase is disclosed. The process further comprises recycling of part of liquid products (HVGO) along with fresh heavy oil for improving the product selectivity. This recycled HVGO is having high concentrations of aromatics compounds. The separation of particles generated during the reaction at reactor exit also avoids the chances of choking of downstream sections.
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公开(公告)号：US20230035683A1
公开(公告)日：2023-02-02
申请号：US17814929
申请日：2022-07-26
发明人： Yamini GUPTA , Arun ARANGARASU , Nepal VISWAKARMA , Ganesh Vitthalrao BUTLEY , Sarvesh KUMAR , Madhusudan SAU , Gurpreet Kapur SINGH , Sankara Sri Venkata RAMAKUMAR
摘要： The present invention provides a multistage single reactor system for hydroprocessing and a process of carrying out multistage hydroprocessing in the said reactor assembly consisting of, a fixed bed solid catalyst system, a feed injection system enabling axial flow of hydrogen saturated hydrocarbon feed, a hydrogen dispensing system inside the reactor enabling minimum required hydrogen flow in cross-flow pattern, also using multitudes of integrated separation and withdrawal limbs for continuous staging. The innovative reactor disclosed in the present invention enables continuous separation and withdrawal of gaseous products along the reactor length by means of combined horizontal reactor orientation and vertical separation limbs provided at the top of the horizontally oriented reactor. The advantage of the reactor assembly includes effective heat sink of exothermic reactions and lower severity of operation due to removal of inhibitory gaseous products.
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10.发明申请公开(公告)号：US20220089960A1
公开(公告)日：2022-03-24
申请号：US17481077
申请日：2021-09-21
发明人： Vasamsetty Naga Veera HIMA BINDU , Mainak SARKAR , Ganesh Vitthalrao BUTLEY , Ramesh KARUMANCHI , Sarvesh KUMAR , Madhusudan SAU , Gurpreet Singh KAPUR , Sankara Sri Venkata RAMAKUMAR
摘要： A process and a system are used for production of multiple grades of ultralow aromatic solvents/chemicals having preferred boiling range, flash point and viscosity from different hydrocarbon streams. A plurality of hydrotreating steps are used to hydrotreat a plurality of hydrocarbon feedstocks in the presence of a hydrogen gas stream and a catalyst system. Further, at least one dissolved gas stripping step, at least one adsorption step, and a distillation step are included in the process. Desired iso-paraffin molecules are thereby preserved, and the undesired aromatic molecules are converted into desired naphthene molecules.
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